Combination of V2O5/WO3−TiO2, Fe−ZSM5, and Cu−ZSM5 Catalysts for the Selective Catalytic Reduction of Nitric Oxide with Ammonia

2008 ◽  
Vol 47 (22) ◽  
pp. 8588-8593 ◽  
Author(s):  
Oliver Kröcher ◽  
Martin Elsener
Fuel ◽  
2021 ◽  
Vol 304 ◽  
pp. 121445
Author(s):  
Running Kang ◽  
Junyao He ◽  
Feng Bin ◽  
Baojuan Dou ◽  
Qinglan Hao ◽  
...  

2005 ◽  
Vol 6 (4) ◽  
pp. 281-285 ◽  
Author(s):  
W. Arous ◽  
H. Tounsi ◽  
S. Djemel ◽  
A. Ghorbel ◽  
G. Delahay

ChemCatChem ◽  
2015 ◽  
Vol 7 (12) ◽  
pp. 1818-1825 ◽  
Author(s):  
Akira Yamamoto ◽  
Kentaro Teramura ◽  
Saburo Hosokawa ◽  
Tetsuya Shishido ◽  
Tsunehiro Tanaka

1970 ◽  
Vol 4 (1) ◽  
Author(s):  
Ismail Mohd Saaid ◽  
Abdul Rahman Mohamed and Subhash Bhatia

Kinetics for the selective catalytic reduction (SCR) of nitric oxide (NO) using i-C4H10 as the reducing agent over Pt-Cu-ZSM5 has been investigated in the temperature range of 200 ?C – 450 oC. Langmuir-Hinshelwood-Hougen-Watson model was proposed for kinetics of the reaction and reaction parameters were evaluated.  The heat of adsorption of NO was found to be considerably high, attributed to strong covalent bond between NO gas molecules and metal active sites.  Using reaction parameters obtained from the experiment, the heterogeneous model could form a good correlation between experimental and simulated values of NO reduction. Key Words: Reaction kinetics, Selective catalytic reduction, NO reduction, Bimetallic catalyst, H-ZSM-5 zeolite.


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